US3574755A - High purity olefin oxide adducts of alkyl and alkenyl amines - Google Patents

High purity olefin oxide adducts of alkyl and alkenyl amines Download PDF

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US3574755A
US3574755A US767464A US3574755DA US3574755A US 3574755 A US3574755 A US 3574755A US 767464 A US767464 A US 767464A US 3574755D A US3574755D A US 3574755DA US 3574755 A US3574755 A US 3574755A
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alkenyl
amine
olefin oxide
carbons
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Robert B Mcconnell
Robert A Swenson
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Enron Chemical Co
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  • Olefin oxide adducts of alkyl and alkenyl primary amines and alkyl and alkenyl trimethylene diamines are commercially available and widely used as surface active agents, emulsifiers, textile aids and for many other uses.
  • olefin oxide adducts of alkyl or alkenyl primary amines a two step process is usually employed.
  • one mole of the alkyl or alkenyl primary amine is reacted with two moles of the olefin oxide, i.e., ethylene oxide.
  • the olefin oxide i.e., ethylene oxide.
  • fatty amines from natural oils such as coco, tallow, soya and tall oils. This reaction proceeds readily by bringing the reactants together and subjecting them to a temperature of about 50 to 200 C.
  • N,N-bis(2-hydroxyethyl)-N-alkyl or alkenyl amine having the formula CHzCHzOH cmomorr
  • the N,N-bis(2-hydroxyethyl)-N-alkyl or alkenyl amine is then reacted, in the second step, with such additional amount of the same olefin oxide, i.e., ethylene oxide, as to form polyethoxyethanol chains of the desired length.
  • This step can be represented as follows:
  • x, y and R have the significance previously assigned and 1: equals x-i-y.
  • a catalyst such as sodium metal, sodium hydroxide and potassium hydroxide is generally employed to promote the reaction.
  • a two step process analogous to that described for the alkyl or alkenyl primary amines, is employed with alkyl or alkenyl trimethylene diamines to form olefin oxide adducts thereof.
  • the nonamine materials present in ethoxylated alkyl or alkenyl primary amines are generally considered to be caused by reaction of ethylene oxide with water present in the system.
  • the presence of water in the system while ethoxylating with a strong basic catalyst also leads to discoloration of the adduct. It is possible to control to some extent the formation of polyethylene glycols during ethoxylation by excluding water from the system. Exclusion of Water from the system, however, does not always give a light colored product, or low nonamine content, when a basic catalyst is used.
  • strongly basic quaternary ammoniurn compounds form during the reaction of ethylene oxide with amines.
  • the rate of formation of these strongly basic compounds generally reaches a maximum between the time two moles of ethylene oxide have reacted with one mole of alkyl or alkenyl primary amine, and about 4 moles of ethylene oxide have reacted per mole of alkyl or alkenyl primary amine. Thereafter, the rate of formation of strong base decreases, and ultimately, as ethoxylation proceeds, no more is formed.
  • Quaternary ammonium bases, and quaternary ammonium hydroxides in particular, are well known to be unstable compounds. Such compounds decompose quantitatively at elevated temperatures to yield a tertiary amine, an olefin, and water. Thus it appears that the formation and decomposition of quaternary bases occur simultaneously during ethoxylation of amines, and that the decomposition products from the quaternary base give rise to discoloration and nonamine impurities. This is illustrated below, in which R is alkyl or alkenyl and R and R are 2-hydroxyethyl groups.
  • impurities Five types of impurities which arise from the formation and decomposition of quaternary ammonium bases have been detected and identified by distillation, gas chromatography, and infrared spectrophotometry in ethoxylated amines.
  • the impurities are alkyl or alkenyl morpholines, alpha olefins, acetaldehyde, vinyl glycol ethers and polyethylene glycols.
  • the secondary hydroxyl groups do not contribute to hydrogen bonding with the tertiary amine because of the greater electronegativity of the oxygen atom in the secondary alcohol and steric hindrance due to the alkyl or alkenyl group adjacent to the hydroxyl group.
  • the tertiary nitrogen atom may also be sterically hindered by the secondary alkanol groups, contributing to the lack of hydrogen bonding.
  • the one to two or more mole adduct of alkyl or alkenyl primary amine and an olefin oxide other than ethylene oxide does not readily form undesirable quaternary bases, such adducts can be reacted with ethylene oxide without discoloration or polyethylene glycol formation.
  • novel olefin oxide adducts of alkyl or alkenyl primary amines and alkyl or alkenyl trimethylene diamines which are much lighter in color and much lower in nonamine content, than prior products.
  • novel intermediates and processes of producing the intermediates and the final products are also provided.
  • the olefin oxide adducts of alkyl or alkenyl primary amines provided by this invention can ,be represented by the formula wherein R is alkyl or alkenyl, usually having a straight chain and having about 6 to 30 carbons, and advisably 8 to 20 carbons, R is a lower alkyl having 1 to 3 carbons, x and y represent numbers not less than 1 and generally not greater than 5 and more advisably not greater than 2, and w and z represent numbers from about 1 to 50 and advisably from about 5 to 30.
  • the alkenyl group represented by R will generally have one, two or three ethylenically unsaturated locations.
  • Particularly suitable compounds appear to be those in which x is 1 and y is a number from 1 to 2, and with R being an alkyl or alkenyl having about 8 to 20 carbons, R being an alkyl having 1 to 2 carbons, and w and z being numbers from 5 to 30.
  • novel olefin oxide adducts of alkyl or alkenyl primary amines can be produced by reacting an alkyl or alkenyl primary amine with at least one mole of an olefin oxide having at least three carbons to produce an alkoxylated alkyl or alkenyl amine which is then reacted with ethylene oxide to produce the desired product.
  • This process can be represented as follows:
  • R, R x, y, w and z have the significance assigned in connection with Formula 1, and wherein M is the moles of reactant and equals x+(y1) and M is the moles of reactant and equals w+z.
  • alkyl and alkenyl primary amines used as starting materials are commercially available materials.
  • amines which can be used are the following:
  • Olefin oxides containing more than three carbons which can be used in practicing the process include propylene oxide, 1,2-epoxybutane and 1,2-epoxypentane.
  • the first step of the process is readily effected by bringing the alkyl or alkenyl primary amine and olefin oxide together, in the absence of water and in an inert atmosphere and subjecting them to an elevated temperature sufficient to form the adduct.
  • a temperature of about 80 to 200 C. is suitable for the reaction.
  • the reaction proceeds at atmospheric pressure although superatmospheric pressures such as up to about 100 psi. can also be used.
  • At least one mole of an olefin oxide containing at least three carbons is reacted with each mole of amine.
  • the use of one mole of an olefin oxide per mole of amine is sufficient to reduce the tendency for quaternary base formation in a subsequently formed two mole adduct.
  • the intermediate, formed as above is reacted with ethylene oxide, or with a mixture of ethylene oxide with an olefin oxide having more than two carbons such as propylene oxide or 1,2- epoxybutane.
  • This reaction is readily effected using the reaction conditions described for the first step; however, a catalyst such as one of those named above is used to promote the reaction.
  • a catalyst such as one of those named above is used to promote the reaction.
  • the product is advisably vacuum stripped and filtered.
  • R, R x and y have the significance assigned in connection with Formula 1 and R R R and R are hydrogen or lower alkyls having 1 to 3 carbons with at least 25% of the groups being hydrogen and advisably at least being hydrogen, and e, f, g and h are numbers from about 1 to 24 and the sum of e-
  • R, R x and y have the significance assigned in connection with Formula 1 and R R R and R are hydrogen or lower alkyls having 1 to 3 carbons with at least 25% of the groups being hydrogen and advisably at least being hydrogen
  • e, f, g and h are numbers from about 1 to 24 and the sum of e-
  • novel olefin oxide adducts of alkyl or alkenyl trimethylene diamines can be represented by the formula wherein R, R x, y, w and z have the significance assigned in connection with Formula 1 and p has the same meaning as x, v has the same meaning as w and equals at least 2 and advisably 3 although the sum can be higher such as a total of 6.
  • reaction between the olefin oxide having at least to form an intermediate adduct which is then reacted with ethylene oxide to form the desired product.
  • This reaction can be represented as follows:
  • R, R p, x, y, v, w and 2 have the significance assigned in connection with Formulas 1 and 2, and M is the moles of reactant and equals p+x+ (y1) and M is the moles of reactant and equals v+w+z.
  • reaction conditions used for each of the steps in producing the olefin oxide adducts of the alkyl or alkenyl trimethylene diamines are the same as those given previously for producing the adducts of the alkyl or alkenyl primary amines.
  • a minimum of two moles of an olefin oxide having at least three carbons are reacted, per mole of diamine, to avoid formation of strong bases and nonamine compounds in the desired final product. It is advisable however to use at least three moles of olefin oxide having at least three carbons, per mole of diamine since this leads to an even better final product lower in nonamines and of even better color.
  • mixtures of ethylene oxide with an alofin oxide having at least three carbons it is also within the scope of this invention to use, in the second step of the process, mixtures of ethylene oxide with an alofin oxide having at least three carbons.
  • one mole of amine could be reacted with 2 moles of propylene oxide, and after the addition of catalyst, a third mole of propylene oxide could be added, followed by the addition of several moles of ethylene oxide.
  • the product would exhibit the benefits of our invention, i.e., light color and low nonamine content.
  • novel products provided herewith will generally have no more than 5% by weight of nonamine impurities and most often have no more than 3% by weight of such impurities.
  • the amine adducts prepared according to our invention and disclosed herein are useful as additives to viscose in rayon spinning to prevent plugging on spinnerettes. They are useful in hair colorants to give level or even dyeing and for emulsifying mineral oil for application to dusting cloths and mops. They are also useful as substantive softening agents on textile mill fabrics.
  • EXAMPLE 1 253 g. (1.25 moles) of a commercial distilled coco amine was charged to a 2 liter pressure reactor equipped with stirrer, gas inlet, exhaust, thermometer, and cooling coils. The amine was sparged with nitrogen, vacuum stripped to remove water, and then heated to 125 C. 145 g. (2.5 moles) of propylene oxide was forced into the reactor over a 3-hour period while it reacted with the amine. When the reaction of the amine with the propylene oxide was completed, the product was vacuum stripped, and 0.55 g. of dry sodium hydroxide was added. The
  • the product was vacuum stripped again, and then 715 g. (16.25 moles) of ethylene oxide was forced into the reactor over a 6 hour period while maintaining the temperature at 125 C.
  • the product was vacuum stripped and filtered and was found to be a clear liquid with color 3 Gardner, which was completely soluble in water.
  • the nonamine content of the product was determined to be 0.4%.
  • the product contained an average of 15.0 moles of combined olefin oxide per mole of amine.
  • Example 2 To compare this product with the product obtained from the conventional method for ethoxylating amines, the process of Example 1 was repeated except that g. (2.5 moles) of ethylene oxide was substituted for propylene oxide in the first step.
  • the final product a 15 mole ethylene oxide adduct of coco amine, had a color of 9+ Gardner and contained 9.5% nonamine.
  • EXAMPLE 2 150 g. (0.55 mole) of commercial distilled stearyl amine was charged to the reactor described in Example 1. The charge was vacuum stripped and heated to C. at which temperature 64 g. (1.1 moles) of propylene oxide was forced in. When the reaction was completed, the product was vacuum stripped, and 0.65 g. of dry sodium hydroxide was added. The product was vacuum stripped again, and then 1160 g. (26.4 moles) of ethylene oxide was forced in over an 8 hour period while maintaining the reaction temperature at C. When the reaction was completed, the product was vacuum stripped and filtered.
  • the product had a color of 3 Gardner, was a solid at room temperature, and a clear liquid at temperatures above its melting point of about 50 C Analysis of the product showed that the nonamine content was 2.5%.
  • the product contained 50.0 moles of combined olefin oxide per mole of amine.
  • a conventional product was made, substituting 48.5 g. (1.1 mole) of ethylene oxide for propylene oxide in the first step.
  • the final product was a 50 mole ethylene oxide adduct of stearyl amine.
  • the product had a Gardner color of 7 and containd 18.5% nonamine.
  • EXAMPLE 3 275 g. of a high quality commercial N-tallow trimethylene diamine was charged into the reactor described in Example 1. The quantity charged represents 0.8 equivalent of primary amine, and 0.825 equivalent of secondary amine, or 0.81 mole of diamine. The amine was sparged with nitrogen, vacuum stripped to remove water, and heated to 125 C. At this temperature the amine was reacted with 141 g. of propylene oxide which represents 2 moles per equivalent of primary amine plus 1 mole per equivalent of secondary amine to a total of 3 moles per mole of N-talloy trimethylene diamine. At the completion of the reaction, the product was vacuum stripped, and 0.16 g. of dry sodium hydroxide was added.
  • a product was similarly prepared as above except that 107 g. of ethylene oxide was substituted for the propylene R1 oxide in the first step.
  • the product contained an average 1O (CHZAZHO)x (CH2HO)B (CHZHO)K H of 25 moles of ethylene oxide per mole of dlamme.
  • the color of the product was 10 Gardner and it contained 11% nonamine. (o112ono ,-1- omonoxomcnon-n.
  • R is an alkyl or alkenyl group contaimn about Compounds of the formulae 6 to 30 carbons
  • R is an alkyl having 1 to 3 c arbons
  • R R R and R are hydrogen or an alkyl having 1 (CHZCHO)X-(CH2OHQO)WH to 3 carbons with at least of the groups being hydrogen
  • e, f, g and h are numbers from about 1 to 24
  • ⁇ and x and y are numbers from 1 to 5.
  • R is an alkyl or alkenyl group containing about 6 to 30 carbons
  • R is an alkyl having 1 to 3 carbons
  • )CHzHOh CHQCHZCDFH p
  • x and y are numbers from 1 to 5 and x+(y1)+p equals at least 2
  • v, w and z are numbers from 1 (CHQCHO)YF(CHZCHZO)IH to 50.
  • methyl, x and p are 1 and y is a number from 1 to 2.
  • R is an alkyl or alkenyl group containing about References Cited 6 to 30 carbons
  • R is an alkyl having 1 to 3 carbons
  • x UNITED STATES PATENTS and y are numbers from 1 to 5
  • w and z are numbers 3 118 000 1/1964 Dupre et al 260 0 from 1 to 50.
  • RN is RAYMOND, ASSIStaHt Examiner derived from coco amine.

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Abstract

DISCLOSED ARE OLEFIN OXIDE ADDUCTS OF ALKYL AND ALKENYL PRIMARY AMINES AND OLEFIN OXIDE ADDUCTS OF ALKYL AND ALKENYL TRIMETHYLENE DIAMINES. THE AMINE IS FIRST REACTED WITH ABOUT ONE TO THREE MOLES OF AN OLEFIN OXIDE CONTAINING AT LEAST THREE CARBONS TO FORM AN INTERMEDIATE WHICH IS THEN REACTED WITH ETHYLENE OXIDE TO FORM THE DESIRED PRODUCTS. THE PRODUCTS ARE SURFACE ACTIVE AGENTS CHARACTERIZED BY LIGHT COLOR AND LOW AMOUNTS OF NONAMINE IMPURITIES.

Description

United States Patent 3,574,755 HIGH PURITY OLEFIN OXIDE ADDUCTS 0F ALKYL AND ALKENYL AMINES Robert B. McConnell and Robert A. Swanson, Janesville, Wis., assignors to Northern Petrochemical Company, Omaha, Nebr. N0 Drawing. Filed Oct. 14, 1968, Ser. No. 767,464 Int. Cl. C070 91/12 US. Cl. 260-584 11 Claims ABSTRACT OF THE DISCLOSURE Disclosed are olefin ox id e adducts of alkyl and alkenyl This invention relates to amine derivatives. More particularly, this invention is concerned with novel olefin oxide adducts of alkyl and alkenyl primary amines and olefin oxide adducts of alkyl and alkenyl trimethylene diamines.
Olefin oxide adducts of alkyl and alkenyl primary amines and alkyl and alkenyl trimethylene diamines are commercially available and widely used as surface active agents, emulsifiers, textile aids and for many other uses. Probably the most widely used of these products are those having the formulae /(CH2CH2O)1 H R-N oH oH 0) H and R CH2CH20)y H \NCH2-CH2CH2-N H(O (31120112): (CH2CH2o)l-H Where R is an alkyl or alkenyl group having from about 6 to 30 carbons, but usually about 8 to carbons, and x, y and z are numbers from about 1 to 50 and usually from about 5 to 30.
In the production of the olefin oxide adducts of alkyl or alkenyl primary amines a two step process is usually employed. In the first step, one mole of the alkyl or alkenyl primary amine is reacted with two moles of the olefin oxide, i.e., ethylene oxide. Usually used are fatty amines from natural oils such as coco, tallow, soya and tall oils. This reaction proceeds readily by bringing the reactants together and subjecting them to a temperature of about 50 to 200 C. In this way an intermediate N,N-bis(2-hydroxyethyl)-N-alkyl or alkenyl amine is produced having the formula CHzCHzOH cmomorr The N,N-bis(2-hydroxyethyl)-N-alkyl or alkenyl amine is then reacted, in the second step, with such additional amount of the same olefin oxide, i.e., ethylene oxide, as to form polyethoxyethanol chains of the desired length. This step can be represented as follows:
ice
wherein x, y and R have the significance previously assigned and 1: equals x-i-y. A catalyst such as sodium metal, sodium hydroxide and potassium hydroxide is generally employed to promote the reaction.
A two step process, analogous to that described for the alkyl or alkenyl primary amines, is employed with alkyl or alkenyl trimethylene diamines to form olefin oxide adducts thereof.
Although olefin oxide adducts of alkyl or alkenyl amines and alkyl or alkenyl trimethylene diamines have been produced as described and used commercially for many years the products are usually dark colored and con- "tain varying amounts of nonamine, or nitrogen-free, irripurities at least some of which are deleterious to optimum performance of the products.
The nonamine materials present in ethoxylated alkyl or alkenyl primary amines are generally considered to be caused by reaction of ethylene oxide with water present in the system. The presence of water in the system while ethoxylating with a strong basic catalyst also leads to discoloration of the adduct. It is possible to control to some extent the formation of polyethylene glycols during ethoxylation by excluding water from the system. Exclusion of Water from the system, however, does not always give a light colored product, or low nonamine content, when a basic catalyst is used.
We have discovered that strongly basic quaternary ammoniurn compounds form during the reaction of ethylene oxide with amines. The rate of formation of these strongly basic compounds generally reaches a maximum between the time two moles of ethylene oxide have reacted with one mole of alkyl or alkenyl primary amine, and about 4 moles of ethylene oxide have reacted per mole of alkyl or alkenyl primary amine. Thereafter, the rate of formation of strong base decreases, and ultimately, as ethoxylation proceeds, no more is formed.
Whe have proposed a structure for the strong base, and the following mechanism for its formation, in which R has the assigned meaning:
olncngorr rt-N-omcmon CH2 5 E o --H---OCH2CHzN-R c112 01120112011 CH2 R-N-CHzCHzOH 5 /O "H-'-OCH2CHzN-R om 01120112011 (DI-120112011 [R-Jf-CHzCHzOH] omomN-R CHzCHzOH 01120112011 quaternary ammonium alkox The quaternary ammonium alkoxide can then rearrange to give a quaternary ammonium hydroxide and an alkyl morpholine:
We have detected the presence of alkyl or alkenyl morpholine compounds in ethoxylated amines, which indicates that quaternary ammonium hydroxide formation does occur during ethoxylation. This is an unusual phenomenon. It is known that quaternary ammonium hydroxides can be produced by ethoxylation of amines in the presence of water; however, one would not expect this to occur in the absence of water. We have found that strong base formation does occur during ethoxylation in the absence of water, and we attribute the formation to the mechanism previously described. The presence of a strong quaternary base in ethoxylated amines is evidenced by the high pH of such compounds, and the quantity of such base may be estimated by titration of the ethoxylated amine with acid solution to the phenolphthalein end point.
Quaternary ammonium bases, and quaternary ammonium hydroxides in particular, are well known to be unstable compounds. Such compounds decompose quantitatively at elevated temperatures to yield a tertiary amine, an olefin, and water. Thus it appears that the formation and decomposition of quaternary bases occur simultaneously during ethoxylation of amines, and that the decomposition products from the quaternary base give rise to discoloration and nonamine impurities. This is illustrated below, in which R is alkyl or alkenyl and R and R are 2-hydroxyethyl groups.
(1) Decomposition of the base can yield acetaldehyde,
which causes discoloration.
(2) Decomposition of the base can yield two types of unsaturated compounds which are present as nonamine impurities.
[momomrs-omomo oH2oH2o),.oH2oH20H OH- A RrCHzCHzlTT 0112 0110 (CH2CH20) CHzCHzOH E Ra vlnyl glycol ether R: A R1CH=CH2 I I-OHzCH20(CH2CH2O) nCHzOHzOH 1120 alpha olefin Rs (3) Water liberated by the decomposition of the base can react with additional ethylene oxide to form polyethylene glycols.
Five types of impurities which arise from the formation and decomposition of quaternary ammonium bases have been detected and identified by distillation, gas chromatography, and infrared spectrophotometry in ethoxylated amines. The impurities are alkyl or alkenyl morpholines, alpha olefins, acetaldehyde, vinyl glycol ethers and polyethylene glycols.
If the formation, or decomposition, of quaternary ammonium bases could be prevented during ethoxylation, a
much purer ethoxylate would result. One way of preventing the decomposition of the base would be to ethoxylate the amine at a temperature sufliciently low that the base is stable. However, when this is done the base is present in the product, and exposure of the product to heat will decompose the base and liberate nonamine impurities. Thus, it would be better to prevent the formation of a quaternary base if possible.
We have discovered that when an alkyl or alkenyl primary amine is reacted with one to two or more moles of an olefin oxide other than ethylene oxide, such as propylene oxide or 1,2-epoxybutane, and the product is then reacted with ethylene oxide, no quaternary base is formed. We attribute this to the fact that these olefin oxides form secondary hydroxyl groups when reacted with an amine, in contrast with ethylene oxide which forms a primary hydroxyl group under the same conditions.
The secondary hydroxyl groups do not contribute to hydrogen bonding with the tertiary amine because of the greater electronegativity of the oxygen atom in the secondary alcohol and steric hindrance due to the alkyl or alkenyl group adjacent to the hydroxyl group. The tertiary nitrogen atom may also be sterically hindered by the secondary alkanol groups, contributing to the lack of hydrogen bonding.
Since the one to two or more mole adduct of alkyl or alkenyl primary amine and an olefin oxide other than ethylene oxide does not readily form undesirable quaternary bases, such adducts can be reacted with ethylene oxide without discoloration or polyethylene glycol formation.
Although the discussion so far has been directed primarily to alkyl or alkenyl primary amines, similar advantageous results are obtained by reacting alkyl or alkenyl trimethylene diamines with two to three or more moles of an olefin oxide other than ethylene oxide and then reacting the resulting adduct with ethylene oxide.
There is accordingly provided by this invention novel olefin oxide adducts of alkyl or alkenyl primary amines and alkyl or alkenyl trimethylene diamines which are much lighter in color and much lower in nonamine content, than prior products. There is also provided novel intermediates and processes of producing the intermediates and the final products.
The olefin oxide adducts of alkyl or alkenyl primary amines provided by this invention can ,be represented by the formula wherein R is alkyl or alkenyl, usually having a straight chain and having about 6 to 30 carbons, and advisably 8 to 20 carbons, R is a lower alkyl having 1 to 3 carbons, x and y represent numbers not less than 1 and generally not greater than 5 and more advisably not greater than 2, and w and z represent numbers from about 1 to 50 and advisably from about 5 to 30. The alkenyl group represented by R will generally have one, two or three ethylenically unsaturated locations. Particularly suitable compounds appear to be those in which x is 1 and y is a number from 1 to 2, and with R being an alkyl or alkenyl having about 8 to 20 carbons, R being an alkyl having 1 to 2 carbons, and w and z being numbers from 5 to 30.
The novel olefin oxide adducts of alkyl or alkenyl primary amines can be produced by reacting an alkyl or alkenyl primary amine with at least one mole of an olefin oxide having at least three carbons to produce an alkoxylated alkyl or alkenyl amine which is then reacted with ethylene oxide to produce the desired product. This process can be represented as follows:
wherein R, R x, y, w and z have the significance assigned in connection with Formula 1, and wherein M is the moles of reactant and equals x+(y1) and M is the moles of reactant and equals w+z.
The alkyl and alkenyl primary amines used as starting materials are commercially available materials. Among such amines which can be used are the following:
n-octylamine palmitylamine n-decylamine tallow amine cocoamine soya amine laurylamine stearylamine myristylamine oleylamine Olefin oxides containing more than three carbons which can be used in practicing the process include propylene oxide, 1,2-epoxybutane and 1,2-epoxypentane.
The first step of the process is readily effected by bringing the alkyl or alkenyl primary amine and olefin oxide together, in the absence of water and in an inert atmosphere and subjecting them to an elevated temperature sufficient to form the adduct. Usually a temperature of about 80 to 200 C. is suitable for the reaction. The reaction proceeds at atmospheric pressure although superatmospheric pressures such as up to about 100 psi. can also be used. At least one mole of an olefin oxide containing at least three carbons is reacted with each mole of amine. The use of one mole of an olefin oxide per mole of amine is sufficient to reduce the tendency for quaternary base formation in a subsequently formed two mole adduct. This means that the subsequent addition of ethylene oxide does not produce discoloration and nonamine formation to anywhere near the extent as when the amine adduct is prepared from ethylene oxide alone. However, it is recommended to use more than one mole of an olefin oxide having at least three carbons to react with one mole of amine. Usually, most satisfactory results are obtained with two or more moles of olefin oxide per mole of amine. No catalyst is required to effect the reaction of up to two moles of an olefin oxide having at least three carbons with each mole of amine; however, greater amounts of olefin oxide require use of a catalyst such as metallic sodium, sodium hydroxide, potassium hydroxide and sodium methylate.
three carbons and the alkyl or alkenyl primary amine proceeds quickly and is usually substantially completed in about one to five hours. The resulting intermediate is then advisably vacuum stripped.
In the second step of the process the intermediate, formed as above, is reacted with ethylene oxide, or with a mixture of ethylene oxide with an olefin oxide having more than two carbons such as propylene oxide or 1,2- epoxybutane. This reaction is readily effected using the reaction conditions described for the first step; however, a catalyst such as one of those named above is used to promote the reaction. After the reaction has been terminated the product is advisably vacuum stripped and filtered.
It is also suitable in the second step of the reaction to employ a mixture of an olefin oxide having at least three carbons, such as propylene oxide or 1,2-epoxybutane, with ethylene oxide. However, when such mixtures are used it is advisable to employ at least one mole of ethylene oxide per each mole of an olfin oxide having at least three carbons. The products obtained from such a reaction can be represented by the formula wherein R, R x and y have the significance assigned in connection with Formula 1 and R R R and R are hydrogen or lower alkyls having 1 to 3 carbons with at least 25% of the groups being hydrogen and advisably at least being hydrogen, and e, f, g and h are numbers from about 1 to 24 and the sum of e-|-f+g+lz is about 4 to 96. It should be understood that the order of the alkoxy groups in the chains, other than those bonded directly to the nitrogen, will be random and will probably not repeat in any set pattern. However, the average number and type of alkoxy groups in each chain can be expected to be proportional to the particular moles of olefin oxide used in the reacting mixture.
No special reaction conditions need be used with olefin oxide mixtures since good results can be obtained using substantially the same conditions as are specified herein for the use of only ethylene oxide in the second step.
There is also provided by this invention novel olefin oxide adducts of alkyl or alkenyl trimethylene diamines. These products can be represented by the formula wherein R, R x, y, w and z have the significance assigned in connection with Formula 1 and p has the same meaning as x, v has the same meaning as w and equals at least 2 and advisably 3 although the sum can be higher such as a total of 6.
The reaction between the olefin oxide having at least to form an intermediate adduct which is then reacted with ethylene oxide to form the desired product. This reaction can be represented as follows:
wherein R, R p, x, y, v, w and 2 have the significance assigned in connection with Formulas 1 and 2, and M is the moles of reactant and equals p+x+ (y1) and M is the moles of reactant and equals v+w+z.
The reaction conditions used for each of the steps in producing the olefin oxide adducts of the alkyl or alkenyl trimethylene diamines are the same as those given previously for producing the adducts of the alkyl or alkenyl primary amines. However, in the first step a minimum of two moles of an olefin oxide having at least three carbons are reacted, per mole of diamine, to avoid formation of strong bases and nonamine compounds in the desired final product. It is advisable however to use at least three moles of olefin oxide having at least three carbons, per mole of diamine since this leads to an even better final product lower in nonamines and of even better color.
It is also within the scope of this invention to use, in the second step of the process, mixtures of ethylene oxide with an alofin oxide having at least three carbons. Conversely, in order to obtain the proper balance of properties in an olefin oxide-amine adduct, it may be desirable to add more than three moles of propylene oxide or 1,2- epoxybutane per mole of alkyl or alkenyl ethylene diamine before adding ethylene oxide. For instance, one mole of amine could be reacted with 2 moles of propylene oxide, and after the addition of catalyst, a third mole of propylene oxide could be added, followed by the addition of several moles of ethylene oxide. The product would exhibit the benefits of our invention, i.e., light color and low nonamine content.
The novel products provided herewith will generally have no more than 5% by weight of nonamine impurities and most often have no more than 3% by weight of such impurities.
The amine adducts prepared according to our invention and disclosed herein are useful as additives to viscose in rayon spinning to prevent plugging on spinnerettes. They are useful in hair colorants to give level or even dyeing and for emulsifying mineral oil for application to dusting cloths and mops. They are also useful as substantive softening agents on textile mill fabrics.
EXAMPLE 1 253 g. (1.25 moles) of a commercial distilled coco amine was charged to a 2 liter pressure reactor equipped with stirrer, gas inlet, exhaust, thermometer, and cooling coils. The amine was sparged with nitrogen, vacuum stripped to remove water, and then heated to 125 C. 145 g. (2.5 moles) of propylene oxide was forced into the reactor over a 3-hour period while it reacted with the amine. When the reaction of the amine with the propylene oxide was completed, the product was vacuum stripped, and 0.55 g. of dry sodium hydroxide was added. The
product was vacuum stripped again, and then 715 g. (16.25 moles) of ethylene oxide was forced into the reactor over a 6 hour period while maintaining the temperature at 125 C. The product was vacuum stripped and filtered and was found to be a clear liquid with color 3 Gardner, which was completely soluble in water. The nonamine content of the product was determined to be 0.4%. The product contained an average of 15.0 moles of combined olefin oxide per mole of amine.
To compare this product with the product obtained from the conventional method for ethoxylating amines, the process of Example 1 was repeated except that g. (2.5 moles) of ethylene oxide was substituted for propylene oxide in the first step. The final product, a 15 mole ethylene oxide adduct of coco amine, had a color of 9+ Gardner and contained 9.5% nonamine.
EXAMPLE 2 150 g. (0.55 mole) of commercial distilled stearyl amine was charged to the reactor described in Example 1. The charge was vacuum stripped and heated to C. at which temperature 64 g. (1.1 moles) of propylene oxide was forced in. When the reaction was completed, the product was vacuum stripped, and 0.65 g. of dry sodium hydroxide was added. The product was vacuum stripped again, and then 1160 g. (26.4 moles) of ethylene oxide was forced in over an 8 hour period while maintaining the reaction temperature at C. When the reaction was completed, the product was vacuum stripped and filtered. The product had a color of 3 Gardner, was a solid at room temperature, and a clear liquid at temperatures above its melting point of about 50 C Analysis of the product showed that the nonamine content was 2.5%. The product contained 50.0 moles of combined olefin oxide per mole of amine.
A conventional product was made, substituting 48.5 g. (1.1 mole) of ethylene oxide for propylene oxide in the first step. The final product was a 50 mole ethylene oxide adduct of stearyl amine. The product had a Gardner color of 7 and containd 18.5% nonamine.
EXAMPLE 3 275 g. of a high quality commercial N-tallow trimethylene diamine was charged into the reactor described in Example 1. The quantity charged represents 0.8 equivalent of primary amine, and 0.825 equivalent of secondary amine, or 0.81 mole of diamine. The amine was sparged with nitrogen, vacuum stripped to remove water, and heated to 125 C. At this temperature the amine was reacted with 141 g. of propylene oxide which represents 2 moles per equivalent of primary amine plus 1 mole per equivalent of secondary amine to a total of 3 moles per mole of N-talloy trimethylene diamine. At the completion of the reaction, the product was vacuum stripped, and 0.16 g. of dry sodium hydroxide was added. The product was vacuum stripped again, and then 785 g. of ethylene oxide was added to the initial 3-mole propylene oxide adduct 6. Compounds according to claim 3 in which R-N is over a 6 hour period while maintaining the reaction temderived from tallow amine. perature at 125 C. The product was vacuum stripped and 7. Compounds according to claim 3 in which R-N is filtered. The product contained an average of 25 moles of derived from soya amine.
combined olefin oxide per mole of diamine and was clear liquid with color 3 Gardner. The nonamine content of the product was 1.8%.
A product was similarly prepared as above except that 107 g. of ethylene oxide was substituted for the propylene R1 oxide in the first step. The product contained an average 1O (CHZAZHO)x (CH2HO)B (CHZHO)K H of 25 moles of ethylene oxide per mole of dlamme. The color of the product was 10 Gardner and it contained 11% nonamine. (o112ono ,-1- omonoxomcnon-n The foregoing detailed description has been given for clearness of understanding only, and no unnecessary limi- 15 tations should be understood therefrom, as modifications will be obvious to those skilled in the art.
What is claimed is:
wherein R is an alkyl or alkenyl group contaimn about Compounds of the formulae 6 to 30 carbons, R is an alkyl having 1 to 3 c arbons, R R R and R are hydrogen or an alkyl having 1 (CHZCHO)X-(CH2OHQO)WH to 3 carbons with at least of the groups being hydrogen, e, f, g and h are numbers from about 1 to 24,
\ and x and y are numbers from 1 to 5.
(CHz(|lHO)y1( 9. Compounds according to claim 8 in which R is 8. Compounds of the formula R1 25 methyl, x is 1 and y is a number from 1 to 2.
I'M R (CH2CHO) (OH2CH20)w-H /NC H2 C H2 0 H2N\ H(0cH2CH2)v (OCHCH2)p (CHflfiHOh-r-(OHzCHzOh-H I ll R1 wherein R is an alkyl or alkenyl group containing about compounds f t e formula 6 to carbons, R is an alkyl having 1 to 3 carbons, Rl p, x and y are numbers from 1 to 5 and in the second R (015mlJ HmHCHZCHNMH formula x+(y-l)+p equals at least 2, and v, w and z are numbers from 1 to 50.
2. Compounds of the formula wherein R is an alkyl or alkenyl group containing about 6 to 30 carbons, R is an alkyl having 1 to 3 carbons, )CHzHOh (CHQCHZCDFH p, x and y are numbers from 1 to 5 and x+(y1)+p equals at least 2, and v, w and z are numbers from 1 (CHQCHO)YF(CHZCHZO)IH to 50.
11. Compounds according to claim 10 in which R; is
methyl, x and p are 1 and y is a number from 1 to 2.
wherein R is an alkyl or alkenyl group containing about References Cited 6 to 30 carbons, R is an alkyl having 1 to 3 carbons, x UNITED STATES PATENTS and y are numbers from 1 to 5 and w and z are numbers 3 118 000 1/1964 Dupre et al 260 0 from 1 to 50. 3. Compounds according to claim 2 in which R is an $3 5? 23 alkyl or alkenyl group containing about 8 to 20 carbons, I R is methyl, x is 1, y is a number from 1 to 2 and w CHARLES R PARKER Primary Examiner and z are numbers from 5 to 30.
4. Compounds according to claim 3 in which RN is RAYMOND, ASSIStaHt Examiner derived from coco amine.
5. Compounds according to claim 2 in which R-N is 0 derived from stearyl amine 252-182; 260-247, 567.6, 501, 615
P0405) UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 3,574,755 Dated April 13, 1971 Inventor) Robert B. McConnell and Robert A. Swenson It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:
Column 3, line 55 "v1yn1 should be --vinyl-- Column 7 line 42 "aLIo Enfl should be --o1efin-- Column 9 line 26 insert the word --andbetween the formulas line 6 "clalm 2" should have been --claim 3- Signed and sealed this 1 7th day of August 1 971 (SEAL) Attest:
EDWARD 'M.FLETGI-ER,J'R. WILLIAM E. SCHUYLER, Attesting Officer Commissioner of Patenl
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US4049557A (en) * 1972-07-17 1977-09-20 Colgate-Palmolive Company Fabric conditioning compositions
US4130589A (en) * 1974-12-11 1978-12-19 Sandoz Ltd. Oxyalkylated alkyl polyamines as defoaming agents
US4256802A (en) * 1979-06-11 1981-03-17 The Upjohn Company Process for polyisocyanurate foams suitable for panels
DE3046352A1 (en) * 1979-12-10 1981-09-10 Berol Kemi AB, 44401 Stenungsund Boundary-active quaternary ammonium compounds and their use for the treatment of textile and cellulose materials
US4511516A (en) * 1980-06-12 1985-04-16 Union Oil Company Of California Boron containing heterocyclic compounds
US4827038A (en) * 1987-08-03 1989-05-02 Texaco Inc. Bis(diaminopolyalkoxy)-N-alkylamines by amination of hydroxyl-containing tertiary amines
US4981609A (en) * 1980-06-19 1991-01-01 Petrolite Corporation Compounds containing sulfur and amino groups
US5068431A (en) * 1987-08-31 1991-11-26 Witco Corporation Methods of making new surface active compounds
US5226943A (en) * 1986-08-20 1993-07-13 Akzo N.V. Herbicides and fungicides containing activity promoting additives
US5366737A (en) * 1985-01-07 1994-11-22 Syntex (U.S.A.) Inc. N-[ω,(ω-1)-dialkyloxy]- and N-[ω,(ω-1)-dialkenyloxy]-alk-1-yl-N,N,N,-tetrasubstituted ammonium lipids and uses therefor
US5545412A (en) * 1985-01-07 1996-08-13 Syntex (U.S.A.) Inc. N-[1, (1-1)-dialkyloxy]-and N-[1, (1-1)-dialkenyloxy]-alk-1-yl-n,n,n-tetrasubstituted ammonium lipids and uses therefor
US5696291A (en) * 1991-11-01 1997-12-09 Witco Corporation Cationic polyurethane compositions, quaternary ammonium salts and methods for their preparation
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US20170129848A1 (en) * 2011-11-22 2017-05-11 Taminco Bvba Stabilized choline solutions and methods for preparing the same

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US4049557A (en) * 1972-07-17 1977-09-20 Colgate-Palmolive Company Fabric conditioning compositions
US4130589A (en) * 1974-12-11 1978-12-19 Sandoz Ltd. Oxyalkylated alkyl polyamines as defoaming agents
US4256802A (en) * 1979-06-11 1981-03-17 The Upjohn Company Process for polyisocyanurate foams suitable for panels
DE3046352A1 (en) * 1979-12-10 1981-09-10 Berol Kemi AB, 44401 Stenungsund Boundary-active quaternary ammonium compounds and their use for the treatment of textile and cellulose materials
US4511516A (en) * 1980-06-12 1985-04-16 Union Oil Company Of California Boron containing heterocyclic compounds
US4981609A (en) * 1980-06-19 1991-01-01 Petrolite Corporation Compounds containing sulfur and amino groups
US5622712A (en) * 1985-01-07 1997-04-22 Syntex (U.S.A.) Inc. N-[ω, (ω-1)-dialkyloxy]- and N-[ω, (ω-1)-dialkenyloxy]-alk-1-yl-N, N, N-tetrasubstituted ammonium lipids and uses therefor
US6387395B1 (en) * 1985-01-07 2002-05-14 Deborah A. Eppstein N-[1, (1-1) -dialkyloxy] - and N- [1, (1-1) -dialkenyloxy]- alk-1-yl-N,N,N-tetrasubstituted ammonium lipids and uses therefor
US5366737A (en) * 1985-01-07 1994-11-22 Syntex (U.S.A.) Inc. N-[ω,(ω-1)-dialkyloxy]- and N-[ω,(ω-1)-dialkenyloxy]-alk-1-yl-N,N,N,-tetrasubstituted ammonium lipids and uses therefor
US5545412A (en) * 1985-01-07 1996-08-13 Syntex (U.S.A.) Inc. N-[1, (1-1)-dialkyloxy]-and N-[1, (1-1)-dialkenyloxy]-alk-1-yl-n,n,n-tetrasubstituted ammonium lipids and uses therefor
US5550289A (en) * 1985-01-07 1996-08-27 Syntex (U.S.A.) Inc. N-(1,(1-1)-dialkyloxy)-and N-(1,(1-1)-dialkenyloxy alk-1-yl-N-N,N-tetrasubstituted ammonium lipids and uses therefor
US5226943A (en) * 1986-08-20 1993-07-13 Akzo N.V. Herbicides and fungicides containing activity promoting additives
US4827038A (en) * 1987-08-03 1989-05-02 Texaco Inc. Bis(diaminopolyalkoxy)-N-alkylamines by amination of hydroxyl-containing tertiary amines
US5068431A (en) * 1987-08-31 1991-11-26 Witco Corporation Methods of making new surface active compounds
US5696291A (en) * 1991-11-01 1997-12-09 Witco Corporation Cationic polyurethane compositions, quaternary ammonium salts and methods for their preparation
EP0945378A2 (en) * 1998-03-23 1999-09-29 Ricoh Company, Ltd. Sheet guide device with sheet position adjusting mechanism and image forming apparatus using the same device
EP0945378A3 (en) * 1998-03-23 2000-08-30 Ricoh Company, Ltd. Sheet guide device with sheet position adjusting mechanism and image forming apparatus using the same device
US6279900B1 (en) 1998-03-23 2001-08-28 Ricoh Company, Ltd. Sheet guide device with sheet position adjusting mechanism and image forming apparatus using the same device
US20100204519A1 (en) * 2007-09-27 2010-08-12 Sanyo Chemical Industries, Ltd. Aliphatic amine alkylene oxide adduct
US8404899B2 (en) * 2007-09-27 2013-03-26 Sanyo Chemical Industries, Ltd. Aliphatic amine alkylene oxide adduct
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